Method and Apparatus for Addition of an Alkali Metal Promoter to a Dehydrogenation Catalyst

ABSTRACT

An apparatus and method for adding an alkali metal promoter into steam and contacting the solution with a dehydrogenation catalyst during a dehydrogenation reaction is disclosed. The apparatus has a first conduit capable of transporting an alkali metal salt solution and a second conduit in fluid communication with the first conduit, the second conduit capable of transporting steam so that the alkali metal salt is dissipated into the steam prior to entry into a dehydrogenation reaction zone.

BACKGROUND OF THE INVENTION

1. Field of the Invention

This invention relates generally to catalytic dehydrogenation reactions,such as the dehydrogenation of alkyl aromatic compounds to produce vinylaromatics, for example ethylbenzene into styrene.

2. Description of the Related Art

Alkenyl aromatics, such as vinyl aromatics, are important compounds usedin the manufacture of many of today's products. These compounds arecommonly produced by catalytic dehydrogenation reactions. For example,styrene can be produced by the catalytic dehydrogenation ofethylbenzene.

Processes for the catalytic dehydrogenation of compounds are well knownin the art. An example is the dehydrogenation of an alkyl aromaticcompound to yield a corresponding alkenyl aromatic compound. Anotherexample is the dehydrogenation of a mono-olefin to yield a correspondingconjugated di-olefin. Many dehydrogenation catalysts and operatingparameters are known, and each can have different advantages anddisadvantages. The dehydrogenation catalysts customarily used in suchprocesses are iron oxide based catalysts.

There are a number of factors to consider relative to dehydrogenationcatalysts and their particular operation, such as for example betweenthe level of conversion and the useful catalyst life. Catalyst life isan important consideration in dehydrogenation reactions. There are thecosts related to the catalyst itself, such as the unit cost of thecatalyst, the useful life of the catalyst, the ability to regenerateused catalyst, and the cost of disposing of used catalyst. There arealso the costs related to shutting down a dehydrogenation reactor toreplace the catalyst and/or to regenerate the catalyst bed, whichincludes labor, materials, and loss of productivity.

Normal catalyst deactivation can tend to reduce the level of conversion,the level of selectivity, or both, each of which can result in anundesirable loss of process efficiency. There can be various reasons fordeactivation of dehydrogenation catalysts. These can include theplugging of catalyst surfaces, such as by coke or tars, which can bereferred to as carbonization; the physical breakdown of the catalyststructure; and, the loss of promoters, such as the physical loss of analkali metal compound from the catalyst. Depending upon the catalyst andthe various operating parameters that are used, one or more of thesemechanisms may apply.

It is generally preferred to maximize the useful catalyst life, andthere are a number of techniques or methods that are known. Onetechnique that is sometimes employed is to raise the reactiontemperature. This can be accomplished, for example, by increasing thetemperature of the reactant stream or by adding heat to the reactorchamber. Such a reaction temperature increase will generally increasethe rate of reaction, which can offset the deactivation of the catalyst,but may also have undesirable results such as harming efficiency orselectivity. There can also be narrow limits to the utility of thistemperature-raising technique. There may also be a mechanicaltemperature limit of the catalyst or the equipment, beyond which furthertemperature increases can degrade the catalyst's physical structureand/or the equipment's integrity. As this limit is approached, thecatalyst would then need to be either replaced or regenerated byconventional ways. Conventional practice generally involves shuttingdown the reactor and physically removing the catalyst for replacement.

It would be desirable to have a catalyst regeneration method that couldbe used during steady-state process conditions without processinterruption, which would maintain acceptable levels of conversion andselectivity. It is also desirable to have an apparatus to facilitate theaddition of the catalyst life extender to the process duringsteady-state process conditions without process interruption.

SUMMARY

One embodiment of the present invention is an apparatus for vaporizingan alkali metal salt into steam having a first conduit capable oftransporting an alkali metal salt solution, the first conduit having atleast one opening through which the solution can exit the first conduit.A second conduit is in fluid communication with the first conduit, thesecond conduit capable of transporting a stream comprising steam,wherein as the alkali metal salt solution exits the first conduit it isdissipated into the steam forming a solution of alkali metal salt insteam.

In an aspect, the apparatus has at least one diffuser located adjacentto the opening of the first conduit to dissipate the alkali metal saltsolution into the steam. The second conduit can be connected to a thirdconduit for transporting the vaporized alkali metal salt in steam into astream within the third conduit. The stream located within the thirdconduit can also contain reactants for a dehydrogenation reaction of analkyl aromatic hydrocarbon. The apparatus may further have a weirlocated adjacent to the connection to the third conduit to restrict theflow of any of the alkali metal that is not dissipated into the steamfrom entering the third conduit. The portion of the second conduitcontaining the opening of the first conduit can form a mixing chamberwherein the alkali metal stream can be dissipated into the steam to forma third stream prior to the third stream entering the third conduit. Theportion of the first conduit can be disposed within the second conduitin a substantially concentric arrangement. The alkali metal salt can beadded as a solid, liquid, or a vapor, or a combination thereof.

Another embodiment concerns a method of enhancing the activity of adehydrogenation catalyst promoted with an alkali metal, during acatalytic dehydrogenation reaction. The method includes forming a firstsolution by adding an alkali metal salt to steam utilizing an apparatusfor adding the alkali metal salt into the steam. The apparatus has afirst conduit capable of transporting a first stream of the alkali metalsalt, the first conduit having at least one opening through which thefirst stream can exit the first conduit. A second conduit is in fluidcommunication with the first conduit; wherein the second conduit iscapable of transporting a second stream comprising steam. The firststream exits the first conduit and is dissipated into the second streamforming the first solution containing alkali metal salt of the firststream in solution with the steam of the second stream. The firstsolution is brought into contact with the dehydrogenation catalyst.

The alkali metal salt can be added in amounts sufficient to maintainsubstantially constant levels of catalyst activity, and in an aspect isa potassium salt compound. The catalytic dehydrogenation reaction can bethe dehydrogenation of an alkyl aromatic hydrocarbon reactant stream toobtain an alkenyl aromatic hydrocarbon. The alkali metal salt can beadded to the steam stream as a solid, liquid, or vapor, or a combinationthereof. In an embodiment, the catalyst contains about 40-80 wt % ironoxide and about 5-30 wt % of an alkali metal compound. The alkali metalsalt can be added in amounts equivalent to a continuous addition ofabout 0.01 to about 1000 parts per million by weight of alkali metalrelative to the weight of the total reactant stream. In an embodiment,the alkyl aromatic hydrocarbon is ethylbenzene and the alkenyl aromatichydrocarbon is styrene.

Yet another embodiment concerns a method of revamping an existingfacility used for the dehydrogenation of ethylbenzene to make styreneutilizing a potassium promoted iron based catalyst. The method involvesadding an apparatus to a steam input stream for vaporizing an alkalimetal salt into the steam input stream. The apparatus has a firstconduit capable of transporting an alkali metal salt, the first conduithaving at least one opening through which the alkali metal salt can exitthe first conduit. A second conduit is in fluid communication with thefirst conduit, wherein the second conduit capable of transporting asteam input stream. As the alkali metal salt exits the first conduit itis dissipated into the steam input stream forming a third streamcontaining vaporized alkali metal salt in solution with the steam. Theportion of the first conduit containing the opening can be disposedwithin the second conduit in a substantially concentric arrangement. Theapparatus may have at least one diffuser located adjacent to the openingof the first conduit to dissipate the first stream into the secondstream. The second conduit of the apparatus may be connected to a thirdconduit for transporting the third stream into contact with a fourthstream within the third conduit and can further comprise a weir locatedadjacent to the connection of the second conduit to the third conduit torestrict the flow of any of the alkali metal that is not dissipated intothe second stream from entering the third conduit.

Still another embodiment is an apparatus for supplying a potassiumcarboxylate catalyst life extender to a reaction chamber loaded with aniron oxide based, alkali metal promoted, dehydrogenation catalyst usedto prepare a vinyl aromatic hydrocarbon from a feed stream including analkyl aromatic hydrocarbon. The apparatus has a first conduit capable oftransporting a first stream of a potassium carboxylate, the firstconduit having at least one opening through which the first stream canexit the first conduit. At least a portion of the first conduitcontaining the at least one opening is disposed within a second conduitcapable of transporting a second stream comprising steam. As the firststream exits the first conduit it is dissipated into the second streamforming a third stream containing vaporized potassium carboxylate of thefirst stream in solution with the steam of the second stream.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 is an illustration of an embodiment of the apparatus of thepresent invention for vaporizing an alkali metal salt into steam.

DETAILED DESCRIPTION

Promoted iron oxide catalysts have been found to be especially useful inthe dehydrogenation of alkyl aromatic hydrocarbons to alkenyl aromatichydrocarbons. For example, the production of styrene by thedehydrogenation of ethylbenzene is commonly conducted by mixingethylbenzene with steam, and passing the mixture through adehydrogenation catalyst-packed bed. Typically, compounds of an alkalimetal, such as potassium, will be present in the dehydrogenationcatalyst. The potassium can tend to diminish the deposition of coke onthe catalyst during the dehydrogenation, and thereby increase the usefullife of the catalyst. In an aspect, the potassium may be presenttypically in a quantity of at least 0.01 mole per mole iron oxide up to1 mole per mole iron oxide. One embodiment of a dehydrogenation catalystcontains from about 30 wt % to about 95 wt % iron oxide and about 1 wt %to about 30 wt % of potassium. Another embodiment of a dehydrogenationcatalyst contains from about 40 wt % to about 80 wt % iron oxide andabout 5 wt % to about 20 wt % potassium. Other components may also beadded to the dehydrogenation catalyst to provide further promotion,activation, or stabilization characteristics.

The dehydrogenation of ethylbenzene is usually carried out in thepresence of steam, with the weight ratio of steam:ethylbenzene beingfrom about 0.5:1 to about 4:1, or alternatively from about 0.8:1 toabout 2:1. The steam can serve as a heat transfer medium, and can alsostabilize an intermediate oxidation stage of the catalyst and aid in thegasification of any organic deposits on the catalyst, thus counteringcarbonization of the catalyst. A portion of the organic deposits can beoxidized into carbon monoxide and/or carbon dioxide.

After a fresh load of catalyst or the regeneration of an existingcatalyst, there is typically an initial period of high catalyst activityand selectivity followed by catalyst deactivation. There are a number ofpossible explanations for the gradual deterioration of catalyst activityand one or more mechanisms may apply in a particular process. Onemechanism that may deactivate alkali metal promoted iron-based catalystsis alkali metal loss, wherein the alkali metal is physically releasedfrom the catalyst and becomes entrained with the reactant stream.Another mechanism that may deactivate alkali metal promoted iron-basedcatalysts is alkali metal site contamination, that is, the physicallocation of the alkali metal on the catalyst is covered or otherwiseobstructed, such as by carbonization. As catalyst deactivationprogresses, eventually the level of conversion or selectivity, or both,fall sufficiently low that the dehydrogenation process is no longereconomically viable. At this point the process would typically have tobe shut down and the catalyst either replaced or regenerated byconventional methods.

The present invention involves adding an amount of alkali metal compoundto the process sufficient to regenerate, stabilize, or enhance theactivity of the dehydrogenation catalyst and thereby maintain economicallevels of conversion and selectivity and reduce or delay the need forcatalyst replacement. The alkali metal compound is added to a steaminput stream prior to it entering the process. The alkali metal compoundcan be added in a continuous or intermittent basis as needed and can beutilized in conjunction with other operational techniques such asraising the reaction temperature mentioned above. In one embodiment thealkali metal compound is a potassium compound. In one embodiment thealkali metal compound is a potassium salt compound that can go intosolution with the steam. In alternate embodiments the alkali metalcompound is a lithium compound, a sodium compound, a rubidium compound,a cesium compound, a francium compound, mixtures thereof, and saltsthereof.

In one embodiment the alkali metal compound that is added is an organopotassium salt. A soluble organo potassium salt is put into solutionwith steam before being added to the dehydrogenation process. Apotassium salt can be sprayed or otherwise distributed into a stream ofsteam, for example super heated steam, which can dissolve and/orvaporize the salt and create a steam solution containing the potassiumthat can then be added to the dehydrogenation process. Organo potassiumsalts can vaporize at lower temperatures than non-organo potassiumcompounds, thereby facilitating the distribution of potassium into theflow of steam that is added to the dehydrogenation process. Various waysof putting a salt compound into solution with a liquid or vapor streamare well known in the art, all of which are considered within the scopeof this invention. Non-limiting examples of suitable organo potassiumsalts include potassium acetate, potassium benzoate, potassium citrate,potassium fumarate, potassium gluconate, potassium lactate, potassiummaleate, potassium pamoate, potassium succinate, potassium tartrate, andmixtures thereof. Potassium salt compounds generally have excellentwater solubility, due to the high hydration energy of the K+ ion.

The amount of alkali metal compound added is dependent upon variousfactors such as the amount and purity of the reactant stream, thequantity of catalyst charge, the run length of the catalyst load, thedehydrogenation operating conditions, and the particular catalyst beingtreated. The alkali metal compound can be added in an amount equivalentto a continuous addition of about 0.01 to about 1000 parts per millionby weight of alkali metal relative to the weight of the total reactantstream. In alternate embodiments the alkali metal compound is added inan amount equivalent to a continuous addition of about 0.01 to about750; about 0.10 to about 500; or about 0.1 to about 250 parts permillion by weight of alkali metal relative to the weight of the totalreactant stream. In some embodiments the alkali metal compound is addedin an amount equivalent to a continuous addition of about 0.1 to about100 parts per million by weight of alkali metal relative to the weightof the total reactant stream. U.S. Pat. No. 6,936,743 to Butler, whichis incorporated herein by reference, discloses the addition of acatalyst life extender in amounts equivalent to a continuous addition offrom about 0.01 to about 100 parts per million by weight of the totalalkyl aromatic hydrocarbon directed into the reactor. The alkali metalcompound can also be added in an intermittent manner, and intermittentaddition may be desirable if the amount that is added is so small as tomake continuous addition problematic. In some instances an intermittentaddition of a larger quantity of alkali metal compound may providesuperior results than a continuous addition of a smaller quantity.Variations of the manner in which the alkali metal compound are addedare considered within the scope of this invention.

Referring now to FIG. 1, in one illustrative embodiment 100 an alkalimetal salt is supplied via line 110 and is added to an input stream ofsteam via line 120 where they are combined in a mixing chamber 130 priorto the mixture being added to the dehydrogenation process/apparatus 140.The dehydrogenation process 140 shown herein can be an input stream to adehydrogenation process or can be a portion of the dehydrogenationapparatus, such as a dehydrogenation reaction zone. The alkali metalsalt can be added as a liquid solution, as a solid, or in a vapor phase,or combinations thereof. In an aspect, the steam may be super heated.There may also be various mixing or agitating equipment employed withinthe mixing chamber 130 to facilitate the dissolution of the alkali metalsalt into the steam. In an aspect, the mixing chamber 130 has asubstantially concentric arrangement of the alkali metal salt line 110within the steam line 120, with the streams from the salt line and thesteam line contacting in a con-current flow pattern as shown in FIG. 1.In an alternative embodiment, the mixing chamber 130 has a concentricarrangement of the alkali metal salt line 110 within the steam line 120with the streams from the salt line and the steam line contacting in acounter-current flow pattern, or with the alkali metal salt beingsprayed or otherwise distributed within the mixing chamber 130. Thealkali metal salt line 110 can alternately be attached at an any anglerelative to the mixing chamber 130, such as from zero degrees on oneembodiment having a con-current flow arrangement to 180 degrees on oneembodiment having a counter-current arrangement, or alternatively on a30 degree to 45 degree angle, or may be perpendicular to the mixingchamber 130 with the alkali metal salt being sprayed or otherwisedistributed through an injector head. In the embodiment shown in FIG. 1,there is shown an optional diffuser 150 that can be used to dissipatethe alkali metal salt within the steam stream in the mixing chamber 130.As used herein the term “diffuser” means any apparatus that acts toalter the flow path of the alkali metal salt to assist in itsdissipation within the steam. The diffuser may decelerate the rate offlow, impart turbulence within the flow and/or impart a change indirection of the flow, or a combination thereof. The optional diffuser150 may be of any shape to assist in dissipating the alkali metal saltwithin the steam stream. The diffuser may have an angled or conicalshape, such as shown in FIG. 1, to deflect and distribute the alkalimetal salt in a radial direction within the steam stream. There is alsoshown an optional weir 160 that can be used to restrict the flow of anyalkali metal salt that is not in solution with the steam from enteringthe dehydrogenation process/apparatus 140. As used herein the term“weir” means any apparatus that restricts the flow of any alkali metalsalt that is not in solution with the steam from entering thedehydrogenation process. The weir may inhibit the rate of flow of aportion of the flow that may contain alkali metal salt that is not fullyin solution, such as in one embodiment the lower portion of the flowstream where heavier materials, such as alkali metal salt that is not insolution may settle. The mixture of alkali metal salt and steam can beadded directly to a dehydrogenation reactor or to an input stream of thedehydrogenation process. Other ways of adding the alkali metal to thesteam can include the heating and vaporizing of the alkali metal saltinto the steam stream.

Dehydrogenation catalysts containing iron oxide and alkali metalcompounds are well known in the art and are available commercially fromvarious sources such as: BASF Corporation; Criterion Catalyst Company,L.P.; and Sud Chemie, Inc. These and similar catalysts are consideredwithin the scope of this invention.

As used herein, the term “conversion” means in a quantitative sense thefraction, in % mole, of the reactant that is converted.

The term “selectivity” means the ability of the catalyst to selectivelyproduce higher levels of a desirable product and lower levels of anundesirable product, for example to selectively dehydrogenateethylbenzene to produce styrene instead of toluene or benzene.

The term “activity” means the ability of the catalyst to convert acertain percentage of the reactants for each pass of feedstock over thecatalyst, for example to convert a certain percentage of theethylbenzene to aromatics for each pass of feedstock over the catalyst.

The foregoing description of certain embodiments of the presentinvention has been presented for purposes of illustration anddescription. It is not intended to be exhaustive or limit the inventionto the precise form disclosed, and other and further embodiments of theinvention may be devised without departing from the basic scope thereof.

1-20. (canceled)
 21. An apparatus comprising: a first conduit adapted totransport a first stream of an alkali metal salt, the first conduitcomprising at least one opening through which the first stream can exitthe first conduit; a second conduit in fluid communication with thefirst conduit, wherein the second conduit is adapted to transport asecond stream comprising steam, wherein a portion of the second conduitcontains the at least one opening of the first conduit and is adaptedfor dissipation of the first stream into the second stream to form athird stream; and a weir adapted to restrict a flow of any of alkalimetal salt that is not dissipated into the second stream, wherein theweir is located downstream from the at least one opening of the firstconduit and upstream of a dehydrogenation reaction zone.
 22. Theapparatus of claim 21, further comprising a diffuser located downstreamof the at least one opening of the first conduit, wherein the diffuseris adapted to dissipate the first stream into the second stream.
 23. Theapparatus of claim 22, wherein the diffuser is adapted to decelerate arate of flow of the first stream.
 24. The apparatus of claim 22, whereinthe diffuser is adapted to impart turbulence within the flow of thefirst stream.
 25. The apparatus of claim 22, wherein the diffuser isadapted to impart a change in a direction of the flow of the firststream.
 26. The apparatus of claim 22, wherein the diffuser is adaptedto deflect and distribute the alkali metal salt in a radial directionwithin the second stream.
 27. The apparatus of claim 22, wherein thediffuser has an angled shape.
 28. The apparatus of claim 22, wherein thediffuser has a conical shape.
 29. The apparatus of claim 22, wherein theweir is downstream of the diffuser.
 30. The apparatus of claim 22,wherein the diffuser is located adjacent to the at least one opening ofthe first conduit.
 31. The apparatus of claim 21, wherein the portion ofthe second conduit that contains the at least one opening of the firstconduit forms a mixing chamber.
 32. The apparatus of claim 31, furthercomprising mixing or agitating equipment in the mixing chamber.
 33. Theapparatus of claim 31, wherein the first conduit is at an angle rangingfrom 0 to 180 degrees relative to the mixing chamber.
 34. The apparatusof claim 33, wherein the angle ranges from 30 to 45 degrees.
 35. Theapparatus of claim 31, wherein the first conduit is perpendicular to themixing chamber.
 36. The apparatus of claim 21, wherein the secondconduit is connected to a third conduit adapted to transport the thirdstream into a fourth stream within the third conduit.
 37. The apparatusof claim 36, wherein the weir is located adjacent to the connection ofthe second conduit to the third conduit and is adapted to restrict theflow of any of the alkali metal that is not dissipated into the secondstream from entering the third conduit.
 38. The apparatus of claim 21,wherein the portion of the first conduit containing the at least oneopening is disposed within the second conduit in a substantiallyconcentric arrangement.
 39. A method of revamping an existing facilityfor the dehydrogenation of ethylbenzene to make styrene utilizing apotassium promoted iron based catalyst comprising: adding an apparatusto a steam input stream for vaporizing an alkali metal salt into thesteam input stream, wherein the apparatus comprises: a first conduitadapted to transport a first stream of the alkali metal salt, the firstconduit comprising at least one opening through which the first streamcan exit the first conduit; a second conduit in fluid communication withthe first conduit, wherein the second conduit is adapted to transport asecond stream comprising steam, wherein a portion of the second conduitcontains the at least one opening of the first conduit and is adaptedfor dissipation of the first stream into the second stream to form athird stream; and a weir adapted to restrict a flow of any of alkalimetal salt that is not dissipated into the second stream, wherein theweir is located downstream from the at least one opening of the firstconduit and upstream of a dehydrogenation reaction zone.
 40. The methodof claim 39, wherein the apparatus further comprises a diffuser locateddownstream of the at least one opening of the first conduit, wherein theweir is downstream of the diffuser, and wherein the portion of thesecond conduit that contains the at least one opening of the firstconduit forms a mixing chamber.
 41. An apparatus for supplying apotassium carboxylate catalyst life extender to a reaction chamberloaded with an iron oxide based, alkali metal promoted, dehydrogenationcatalyst used to prepare a vinyl aromatic hydrocarbon from a feed streamincluding an alkyl aromatic hydrocarbon, the apparatus comprising: afirst conduit adapted to transport a first stream of a potassiumcarboxylate, the first conduit having at least one opening through whichthe first stream can exit the first conduit; a second conduit, whereinat least a portion of the first conduit containing the at least oneopening is disposed within the second conduit, wherein the secondconduit is adapted to transport a second stream comprising steam,wherein the apparatus is adapted to dissipated the first stream into thesecond stream as the first stream exits the first conduit, forming athird stream containing vaporized potassium carboxylate in solution withsteam; and a weir adapted to restrict a flow of any of potassiumcarboxylate that is not dissipated into the steam, wherein the weir islocated downstream from the at least one opening of the first conduitand upstream of the reaction chamber.